WO2008058003A2 - Composition et méthode améliorant la qualité des fibres et l'efficacité du processus de production de pâte mécanique - Google Patents

Composition et méthode améliorant la qualité des fibres et l'efficacité du processus de production de pâte mécanique Download PDF

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Publication number
WO2008058003A2
WO2008058003A2 PCT/US2007/083461 US2007083461W WO2008058003A2 WO 2008058003 A2 WO2008058003 A2 WO 2008058003A2 US 2007083461 W US2007083461 W US 2007083461W WO 2008058003 A2 WO2008058003 A2 WO 2008058003A2
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Prior art keywords
pulp
composition
weight percent
formulation
surfactant
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PCT/US2007/083461
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English (en)
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WO2008058003A3 (fr
Inventor
Prasad Y. Duggirala
Sergey M. Shevchenko
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Nalco Company
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Application filed by Nalco Company filed Critical Nalco Company
Priority to CA2668158A priority Critical patent/CA2668158C/fr
Priority to EP07844840.4A priority patent/EP2082093B1/fr
Priority to CN2007800410428A priority patent/CN101535561B/zh
Priority to AU2007317407A priority patent/AU2007317407A1/en
Priority to BRPI0716279-0A2A priority patent/BRPI0716279A2/pt
Publication of WO2008058003A2 publication Critical patent/WO2008058003A2/fr
Publication of WO2008058003A3 publication Critical patent/WO2008058003A3/fr

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    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00—Fibrous raw materials or their mechanical treatment
    • D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/14—Disintegrating in mills
    • D21B1/16—Disintegrating in mills in the presence of chemical agents
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C3/00—Pulping cellulose-containing materials

Definitions

  • the invention relates generally to improving fiber quality and process efficiency in thermomechanical and chemi-thermomechanical pulping. More specifically, the invention relates to using specialty chemical compositions including various combinations of a surfactant, a chelant, and other compounds to improve the mechanical properties and brightness of a paper product produced from a pulp material manufactured in such a process.
  • the invention has particular relevance for decreasing freeness and amount of shives, providing energy and chemical savings, and enhancing brightness and mechanical strength of paper products.
  • Mechanical pulping is a common method to produce inexpensive pulp without a significant loss of mass.
  • Several technologies are currently practiced in mechanical pulping to manufacture products, such as stone ground wood (SGW), pressurized ground wood (PGW), refiner mechanical pulp (RMP), pressurized RMP (PRMP), thermo-RMP (TRMP), thermo-mechanical pulp (TMP), thermo-chemi- mechanical pulp (TCMP), thermo-mechanical-chemi pulp (TMCP), long fiber chemi- mechanical pulp (LFCMP) 5 and chemically treated long fiber (CTLF).
  • SGW stone ground wood
  • PGW pressurized ground wood
  • RMP refiner mechanical pulp
  • PRMP pressurized RMP
  • TRMP thermo-RMP
  • TMP thermo-mechanical pulp
  • TMP thermo-chemi- mechanical pulp
  • TMCP thermo-mechanical-chemi pulp
  • LFCMP long fiber chemi- mechanical pulp
  • CTLFCMP chemically treated long fiber
  • Chelants and surfactants have historically had a place in pulp production. Mechanical pulp production is affected by transitional metal ions found in wood, which promote undesirable side reactions including oxidative reactions that cause yellowing.
  • commodity chelants are used in mechanical pulping processes to immobilize such metal ions.
  • the role of chelants is generally to bind transitional metal cations to prevent their catalytic activity in decomposing bleaching chemicals, such as peroxide, hydrosulfite, and the like.
  • Surfactants have previously been employed in papermaking to accelerate fiber swelling, and to soften and split pulp.
  • JP 05051889 A2 disclosed use of ethylenediaminetetraacetic acid (“EDTA”) and diethylenetriamine pentaacetic acid (“DTPA”) in oxygen treatment of wood pulp (i.e., delignification). Similar combinations used in ozone bleaching of chemical pulps have also been reported (JP 08188976 A2). Combined use of polymeric chelants and surface-active agents was proposed in JP 07138891 A2 for pulp pretreatment before peroxide bleaching.
  • EDTA ethylenediaminetetraacetic acid
  • DTPA diethylenetriamine pentaacetic acid
  • Mechanical pulps typically have low strength. Chemical treatment, such as alkalization, is sometimes used to increase strength, at the expense of brightness. There thus exists a need for economical methods of producing mechanical pulp materials having increased mechanical strength and brightness. In particular, it is desirable to develop a cost-efficient mechanical pulp with improved mechanical strength without sulfonation. Preferably, such a development would combine all components in a single composition. Preserving these pulp properties has been difficult without sacrificing printing properties and yield.
  • the invention provides a composition that decreases freeness and amount of shives, provides energy and chemical savings, and enhances brightness and mechanical strength of a paper product made from a pulp material in a mechanical pulping process.
  • the composition includes one or more surfactants, one or more chelants, and one or more hydrotropes.
  • the composition optionally includes one or more reductive or oxidative pulp modifiers and one or more pH-controlling chemicals.
  • the invention provides a composition that improves a mechanical pulping process.
  • the composition includes an alkyl alcohol alkoxylate surfactant having formula RO[(CH 2 CHCH 3 O) x (CH 2 CH 2 O) ⁇ ]M.
  • R may be a C 4 to C 4 0 straight, branched, or ring alkyl
  • X may be from 0 to about 50
  • Y may be from 1 to about 100
  • M may be H or an alkali metal.
  • the composition optionally includes one or more chelants, one or more hydrotropes, one or more reductive or oxidative pulp modifiers, and one or more pH-controlling chemicals.
  • the invention provides a method of decreasing freeness and amount of shives, providing energy and chemical savings, and enhancing brightness and mechanical strength of a paper product made from a pulp material produced in a mechanical pulping process.
  • the method includes contacting the pulp material with a surfactant composition including an alkyl alcohol alkoxylate surfactant having formula ROt(CH 2 CHCH 3 O) x (CH 2 CH 2 O) Y ]M.
  • R may be from C 4 to C 40 straight, branched, or ring alkyl
  • X may be from 1 to about 50
  • Y may be from 0 to about 100
  • M may be H or an alkali metal.
  • the method further includes optionally introducing to the pulp material separately from the surfactant composition, as part of the surfactant composition, or with the surfactant composition but not as part of the surfactant composition one or more additional formulations.
  • additional formulations include one or more additional surfactants, one or more chelants, one or more hydrotropes, one or more reductive pulp modifiers, one or more oxidative pulp modifiers, one or more pH-controlling chemicals, and combinations thereof.
  • compositions that decrease freeness and amount of shives, provide energy and chemical savings, and enhance brightness and mechanical strength of a paper product produced from a pulp material produced in a mechanical pulping process.
  • a further advantage of the invention is to provide an economical and efficient method of producing a high-quality paper product via a mechanical pulping process.
  • Another advantage of the invention is to provide a method of improving a mechanical pulping process by contacting a pulp material with a surfactant composition and introducing to the pulp material one or more formulations including a pH-controlling chemical at the same stage of the mechanical pulping process; wherein if the pH-controlling chemical is an alkali and is introduced to the pulp material separately from the surfactant composition, the alkali improves the mechanical strength of the paper product without decreasing the brightness of the paper product.
  • Alkyl alcohol means a compound or mixture of compounds having the formula ROH where R is a straight, branched, or ring C 4 to C 40 alkyl group.
  • Alkoxy means an alkyl group attached to the parent molecular moiety through an oxygen atom.
  • Representative alkoxy groups include methoxy, ethoxy, propoxy, butoxy, and the like. Propoxy and ethoxy are preferred.
  • Alkyl means a monovalent group derived from a straight or branched chain or ring saturated hydrocarbon by the removal of a single hydrogen atom.
  • the alkyl may be unsubstituted or substituted with one or more groups selected from amino, alkoxy, hydroxy and halogen.
  • Representative alkyl groups include methyl, ethyl, n- and ⁇ -propyl, n-, sec-, iso- and tert-butyl, and the like.
  • Hydroxide base means hydroxide (OH) salts of alkaline and alkaline earth metals, such as sodium, potassium, lithium, magnesium, calcium, the like, and combinations thereof.
  • Block polymer means the polymer resulting from block addition of more than one different type of monomer, such as propylene oxide and ethylene oxide.
  • Homo polymer means the polymer resulting from the polymerization of one type of monomer, such as propylene oxide or ethylene oxide.
  • Hetero polymer means the polymer resulting from random addition of more than one type of monomer, such as propylene oxide and ethylene oxide.
  • Formulation includes one or more chemicals in solid, powder, crystalline, or other form and/or a solution of one or more chemicals in any suitable solvent in any appropriate concentration.
  • Olet-dry pulp means a paper or pulp that has been dried in an oven, contains practically no moisture, and has constant weight within about 0.1 percent.
  • pH-controIling chemical means any suitable chemical or compound that, when added to a solution, composition, and/or formulation, is capable of adjusting pH, controlling pH, and/or maintaining pH.
  • Active solids means percent of solid active components of a material remaining after drying of a formulation. Inactive admixtures (e.g., sodium chloride) are not considered an active solid.
  • CSF Canadian Standard Freeness as described in TAPPI methods and measured in milliliters.
  • Carboxylic acids means organic compounds containing one or more carboxylic group(s), -C(O)OH, preferably aminocarboxylic acids containing a single C-N bond adjacent (vicinal) to the C- CO 2 H bond, such as: i. EDTA ((HO 2 CCH 2 ) 2 NCH 2 CH 2 N(CH 2 CO 2 H) 2 ), ii. DTPA ((HO 2 CCH 2 ) 2 NCH 2 CH 2 N(CH 2 CO 2 H)CH 2 CH 2 N(CH 2 CO 2 H) 2 ), the like, and alkaline and alkaline earth metal salts thereof.
  • DTPA means diethylenetriamine pentaacetic acid.
  • EDTA means ethylenediaminetetraacetic acid.
  • Dimocarbamates include monomeric dithiocarbamates, polymeric dithiocarbamates, polydiallylamine dithiocarbamates, 2,4,6-trimercapto-l,3,5-triazine, disodium ethylenebisdithiocarbamate, disodium dimethyldithiocarbamate, and the like.
  • Organic phosphates means organic derivatives of phosphorous acid, P(O)(OH) 3 , containing single C-O-P bonds, including triethanolamine triphosphate ester) (N(CH 2 CH 2 OP(O)(OH) 2 )3), and the like.
  • Organic phosphonates means organic derivatives of phosphonic acid, HP(O)(OH) 2 , containing a single C-P bond, such as HEDP (CH 3 C(OH)(P(O)(OH) 2 ), 1 -hydroxy- 1 ,3-propanediylbis-phosphonic acid
  • Sulfites means dibasic metal salts of sulfurous acid, H 2 S ⁇ 3 , including dibasic alkali and alkaline earth metal salts such as sodium sulfite (Na 2 SO 3 ), calcium sulfite (CaSO 3 ), and the like.
  • Bisulfites means monobasic metal salts of sulfurous acid, H 2 SO 3 , including alkali and alkaline earth metal monobasic salts such as sodium bisulfite (NaHSO 3 ), magnesium bisulfite (Mg(HSO 3 ) 2 ), and the like.
  • Metalbisulfites (Pyrosulfites) means salts of pyrosulfurous acid, H 2 S 2 O 5 , including sodium metabisulfite (Na 2 S 2 O 5 ), and the like.
  • Sulfoxylates means salts of sulfoxylic acid, H 2 SO 2 , including zinc sulfoxylate (ZnSO 2 ), and the like.
  • Thiosulfates means salts of thiosulfurous acid, H 2 S 2 O 3 , including potassium thiosulfate (Na 2 S 2 Oj), and the like.
  • Polythionates means salts of polythionic acid, H 2 S n O 6 (n is from 2 to 6), including sodium trithionate (Na 2 S 3 O 6 ), salts of dithionic acid, H 2 S 2 O 6 , such as sodium dithionate Na 2 S 2 O 6 , and the like.
  • Dithionites means salts of dithionous (hydrosulfurous, hyposulfurous) acid, H 2 S 2 O 4 , including sodium dithionite (hydrosulfite) (Na 2 S 2 O 4 ), magnesium dithionite (MgS 2 O 4 ), and the like.
  • Aldehyde bisulfite adducts means compounds of formula R 1 CH(OH)SO 3 H and metal salts thereof where R 1 is selected from alkyl, alkenyl, aryl and arylalkyl.
  • Representative aldehyde bisulfite adducts include formaldehyde bisulfite adduct HOCH 2 SO 3 Na, and the like.
  • Representative sulfnamides include ethylsulfindimethylamide (CH 3 CH 2 S(O)N(CH 3 ) 2 ), and the like.
  • Sulfanamides and ethers of sulfenic acid means compounds of formula R 1 -S-R 2 , where R 1 and R 2 are defined above.
  • Representative sulfenamides include ethylsulfendimethylamide (CH 3 CH 2 SN(CHs) 2 ), and the like.
  • Phosphines means derivatives of phosphine, PH 3 , normally organic substituted phosphines of the formula R 6 R 7 RsP where Re to R 8 are independently selected from hydrogen, alkyl, alkenyl, aryl, arylalkyl (defined below) and NR 4 Rs where R4 and R5 is defined above. Representative phosphines include (HOCEk ⁇ P (THP), and the like.
  • Phosphites means derivatives of phosphorous acid P(OH) 3 , including organic substituted phosphites of the formula (RaO)(R 4 O)(RsO)P where R 3 - R5 are defined above.
  • Representative phosphites include (CH 3 CH 2 O) 3 P, and the like.
  • Thiophosphites means derivatives of phosphorothious acid HSP(OH) 2 , including organic substituted thiophosphites of formula (R 3 O)(R 4 O)(R 5 S)P where R 3 to Rs are defined above.
  • Representative thiophosphites include (CH 3 CH 2 O) 2 (CH 3 CH 2 S)P, and the like.
  • Phosphonium salts means organic substituted phosphines of the formula R 1 R 3 R 4 RsP + X " , where Ri and R 4 to R 5 are as defined above and X is any organic or inorganic anion.
  • Representative phosphonium salts include (HO 2 CCH 2 CH 2 ) 3 P + HCr (THP), [(HOCH ⁇ P + MSO ⁇ (BTHP), and the like.
  • alkenyl means a monovalent group derived from a straight or branched hydrocarbon containing at least one carbon-carbon double bond by the removal of a single hydrogen atom.
  • the alkenyl may be unsubstituted or substituted with one or more groups selected from amino, alkoxy, hydroxyl, and halogen.
  • Alkylene means a divalent group derived from a straight or branched chain saturated hydrocarbon by the removal of two hydrogen atoms, for example methylene, 1,2-ethylene, 1,1 -ethylene, 1,3 -propylene, 2,2- dimethylpropylene, and the like.
  • Aryl means aromatic carbocyclic radicals and heterocyclic radicals having about 5 to about 14 ring atoms.
  • the aryl may be unsubstituted or substituted with one or more groups selected from amino, alkoxy, hydroxy and halogen.
  • Representative aryls include phenyl, naphthyl, phenanthryl, anthracyl, pyridyl, furyl, pyrrolyl, quinolyl, thienyl, thiazolyl, pyrimidyl, indolyl, and the like.
  • Arylalkyl means an aryl group attached to the parent molecular moiety through an alkylene group. Representative arylalkyl groups include benzyl, 2- phenylethyl, and the like.
  • Organic peroxyacid means compounds of formula RiC(O)O 2 H and metal salts thereof where R 1 is selected from alkyl, alkenyl, aryl and arylalkyl.
  • Representative organic peroxyacids include peroxybenzoic acid, CgH 5 C(O)OOH, peracetic acid (PAA), CH 3 C(O)OOH 5 performic acid, HC(O)OOH, perpropionic acid, CH 3 CH 2 C(O)OOH, and the like.
  • Inorganic peroxides means monobasic (hydroperoxides) and dibasic (peroxides) metal derivatives of hydrogen peroxide, H 2 O 2 , including alkali and alkaline earth metal derivatives such as sodium hydroperoxide (NaOOH), magnesium peroxide (MgO 2 ), and the like.
  • Superoxides means metal derivatives containing the group of O 2 " , including alkali and alkaline earth metal derivatives such as sodium superoxide (NaO 2 ), and the like.
  • Periodic-superoxides means mixed alkali metal derivatives of a formula 2MO 2 ⁇ M 2 O 2 , where M is an alkali or alkaline earth metal, such as K 2 O 3 , and the like.
  • Inorganic peroxy acids and salts thereof means inorganic acids containing a -O-O- group, including peroxy monoacids containing the group -OOH and peroxy diacids containing the group -O-O-, and their metal salts, such as peroxymonosulfuric acid (Caro's acid, (HO) 2 SO 2 OOH), peroxydisulfuric acid (HOSO 2 OOSO 2 OH), peroxymonophosphoric acid H 3 PO 5 , sodium peroxymonocarbonate Na 2 CO 4 and peroxydicarbonate Na 2 C 2 Oe, and the like.
  • peroxymonosulfuric acid Caro's acid, (HO) 2 SO 2 OOH
  • peroxydisulfuric acid HOSO 2 OOSO 2 OH
  • peroxymonophosphoric acid H 3 PO 5 sodium peroxymonocarbonate Na 2 CO 4 and peroxydicarbonate Na 2 C 2 Oe, and the like.
  • Periodic peroxides are inorganic salts containing hydrogen peroxide of crystallization, such as sodium metasilicate peroxyhydrate Na 2 SiO 3 *H 2 O 2 »H 2 O, and sodium borate peroxyhydrate NaBO 2 ⁇ H 2 O 2 * 3H 2 O, and the like.
  • Organic peroxides are any organic chemicals containing a -O-O- group, including organic peroxyacids as defined herein, dioxiranes such as dimethyldioxyrane (CHs) 2 CO 2 , and the like.
  • Neitrosodisulfonates are alkali and alkaline earth metal salts of nitrosodisulfonic acid such as potassium nitrosodisulfonate (Fremy's salt) (KSOs) 2 NO, and the like.
  • Hypochlorites are water-soluble metal salts of hypochlorous HOCl, chlorous HOClO, chloric HOClO 2 and perchloric HOCIO3 acids, respectively, such as sodium hypochlorite, NaOCl, and the like.
  • Halpobromites and bromites are water soluble salts of hypobromous acid, HOBr ⁇ and bromic acid, HBrO 3 , respectively, including sodium hypobromite, NaOBr, and the like.
  • Chloroamines and bromoamines are ammonium derivatives of the formulae NH x HaIy, where Hal is Cl or Br, or alkylamine derivatives NRiR 2 HaI x , where Ri and R 2 are defined above and x and y are independently 1 to 3.
  • chloramines and bromoamines may be present as the corresponding ammonium salts.
  • Chloroamides and “bromoamides” are amide derivatives containing -C(O)N(Ri) p HqHal r groups where Hal is defined above, p and q are independently 0 to 1 and r is 1 to 2, such as product compositions formed in a mixture of sodium hypochlorite NaClO and urea H 2 NCONH 2 or sodium hypochlorite NaClO and 5,5-dimethylhydantoin, and the like.
  • Chlorosulfamides and “bromosulfamides” are amide derivatives containing -SO 2 N(Ri ) p H q Hal r , where R 1 , Hal, p, q and r are defined above, such as the product composition formed in a mixture of sodium hypochlorite, NaClO, and sulfamide, H 2 NSO 2 NH 2 , and the like.
  • Activated oxidizing agent means an oxidizing agent used in combination with one or more activators. In some embodiments, the oxidizing agent is activated hydrogen peroxide.
  • the alkyl alcohol alkoxylates of this invention have the formula ROt(CH 2 CHCH 3 O) x (CH 2 CH 2 O) Y ]M.
  • R may be from C 4 to C 40 straight, branched, or ring alkyl
  • X may be from 1 to about 50
  • Y may be from 0 to about 100
  • M may be hydrogen or an alkali metal.
  • the structure of the alkyl alcohol alkoxylate may be a block polymer, a hetero polymer, a homo polymer, or combinations thereof.
  • X is from 1 to 20, Y is from 20 to 80, and M is hydrogen.
  • M is hydrogen.
  • M is potassium.
  • R is a Cg to C 22 alkyl or a C ⁇ alkyl.
  • X is from 1 to 20.
  • Y is from 20 to 80.
  • They are typically prepared by heating a C 4 to C 40 alkyl alcohol, or mixture of C 4 to C 4 o alkyl alcohols (sometimes referred to herein as ROH) with propylene oxide and/or ethylene oxide in the presence of hydroxide base.
  • the ethylene oxide and propylene oxide may be added in random or block fashion, resulting in either a hetero polymer or a block polymer, respectively.
  • the reaction is preferably conducted at a temperature of about 15O 0 C in a pressure vessel at a pressure of about 50 psi to about 75 psi.
  • the alkoxylate product may either be left in salt form or neutralized with acid.
  • Random addition of ethylene oxide and propylene oxide involves simultaneous addition of both components to the alcohol, such that the rate of addition is controlled by their relative amounts and reaction rates.
  • the above formula is not a structural formula. Rather, it is a representation of molar amounts, X and Y, of ethylene oxide and propylene oxide added to the alcohol.
  • X and Y molar amounts
  • X and Y molar amounts
  • the above formula is representative of the structure of the alkoxylated alcohol, except that the (C 2 H 4 O) x and (C 3 ⁇ 6 ⁇ ) ⁇ groups may be reversed, depending on the order of propylene oxide or ethylene oxide addition.
  • the resulting polymer is a highly water-soluble solid.
  • the composition of the invention is an alky] alcohol alkoxylate surfactant having formula ROt(CH 2 CHCH 3 O) x (CH 2 CH 2 O) Y ]M; wherein R is C 4 to C 40 straight, branched, or ring alkyl, X is from 1 to about 50, Y is from 0 to about 100, and M is H or an alkali metal, as explained in more detail above.
  • the composition optionally includes one or more chelants, one or more hydrotropees, one or more reductive or oxidative pulp modifiers, and one or more pH-controlling chemicals (each explained in more detail herein).
  • the composition of the invention in one embodiment, includes an effective amount of a surfactant formulation having one or more surfactants.
  • the role of the surfactants is to improve penetration of liquid or steam into the woodchips thus facilitating homogenization in the mechanical pulping process.
  • surfactants include non-ionic surfactants, alkyl alcohol alkoxylates (as above); block, homo, and hetero polymer alkyl alcohol alkoxylates; ethoxylated tridecyl alcohol; ethoxylated propyloxylated hexadecanol; the like; and combinations thereof.
  • the surfactant formulation typically has from about 0.05 weight percent to about 30 weight percent of one or more surfactants. In a preferred embodiment, the composition has from about 1 weight percent to about 10 weight percent of one or more surfactants.
  • the composition includes surfactant alone and has from about 0.05 weight percent to about 99 weight percent of one or more surfactants.
  • a surfactant only composition has from about 5 weight percent to about 30 weight percent of one or more surfactants.
  • the surfactant only composition has from about 10 weight percent to about 20 weight percent of one or more surfactants.
  • the composition also includes an effective amount of a chelant formulation having one or more chelants.
  • a chelant formulation having one or more chelants.
  • metal ions such as transitional metal ions
  • Chelants efficiently immobilize these ions to prevent such undesirable side reactions.
  • Effective chelants include transitional metal chelants, such as aminocarboxylates, aminophosphonates, polyphosphates, polyacrylates, organic phosphates, organic phosphonates, phosphates, carboxylic acids, the like, and combinations thereof.
  • Preferred chelants include carboxylic acid, phosphonates, DTPA and salts thereof, EDTA and salts thereof, and DTMPA and salts thereof. Typically, about 0.05 weight percent to about 50 weight percent chelant is sufficient. Preferably the chelant is present from about 1 weight percent to about 30 weight percent. Most preferably, the composition includes from about 5 weight percent to about 20 weight percent of one or more chelants.
  • the composition includes an effective amount of a hydrotrope formulation having one or more hydrotropes.
  • Contemplated hydrotropes include arylenesulfonates, such as xylenesulfonate, cumenesulfonate, and toluenesulfonate and carbohydrates having long-chain aliphatic substituents, such as Glucopon® (available from Fitz Chem Corp. in Itasca, IL) and GIucopon®-like compounds.
  • Glucopon compound is Glucopon 425N, D-glucose, decyl ethers, octyl ethers, oligomeric D-glucopyranoside, Qo to Ci 6 alkyloligomeric (available from Cognis Corporation in Hoboken, NJ).
  • the hydrotrope formulation may include any combination of these and similar compounds.
  • the composition has from about 0.05 weight percent to about 50 weight percent of one or more hydrotropes.
  • the composition includes from about 0.05 weight percent to about 50 weight percent of the hydrotrope(s).
  • the composition has from about 5 weight percent to about 30 weight percent hydrotrope.
  • the most preferred hydrotrope content of the composition is from about 10 weight percent to about 20 weight percent.
  • the weight percent ratio of hydrotrope to chelant is typically about one-to-one or greater. In another embodiment, the weight percent ratio of hydrotrope to surfactant is typically about two-to-one or greater.
  • hydrotropes act to increase the aqueous solubility of certain slightly soluble compounds.
  • all the individual components of the invention are soluble in water; however, certain combinations, such as a nonionic surfactant with other, more polar components, may require a wetting agent, such as a hydrotrope to provide compatibility of the composition in a single formulation.
  • a wetting agent such as a hydrotrope
  • a preferred embodiment includes using one or more non-ionic surfactants, which are typically not compatible with chelants.
  • non-ionic surfactants which are typically not compatible with chelants.
  • the non-polar surfactant component precipitates. Incorporating a hydrotrope in the correct ratio (as explained below) maintains solubility of the non-ionic components and thus ensures stability of the composition.
  • a synergistic effect is observed with the addition of a reductive pulp modifier to the composition.
  • reductive pulp modifiers include those compounds that are capable of transforming functional groups in bleached pulp from a higher oxidation category to a lower oxidation category.
  • Representative reductive pulp modifiers include water-soluble inorganic sulfites, bisulfites, metabisulfites, substituted phosphines and tertiary salts thereof, formamidinesulfinic acid and salts and derivatives thereof, formaldehyde bisulfite adduct other aldehyde bisulfite adducts, sulfoxylates, thiosulfates, dithionites, polythionates, sulfinamides and ethers of sulf ⁇ nic acid, sulfenamides and ethers of sulfenic acid, sulfamides, phosphines, phosphonium salts, phosphites, thiophosphites, the like, and combinations thereof.
  • Preferred reductive pulp modifiers include sodium sulfite, bisulfite, and metabisulfite.
  • the effective amount of reductive pulp modifier added to the pulp material is the amount that enhances the brightness and resistance to thermal yellowing in the mechanical pulping of wood that brings increased brightness of the pulp material or paper product compared to untreated pulp material or paper product.
  • about 0.01 to about 50 weight percent of one or more reductive pulp modifiers is effective.
  • a more preferred amount is from about 5 weight percent to about 30 weight percent.
  • the most preferred range is from about 10 weight percent to about 20 weight percent.
  • the composition includes addition of an effective amount of one or more oxidative pulp modifiers.
  • Oxidative pulp modifiers include those chemical substances capable of transforming functional groups in pulp material from a lower oxidation category to a higher oxidation category. Benefits of this transformation include increased brightness and resistance to thermal yellowing in the mechanical pulping of wood that brings higher brightness of the pulp material or paper product compared to untreated pulp material or paper product.
  • Effective amounts of one or more oxidative pulp modifiers are contemplated to be in the range of about 0.01 weight percent to about 50 weight percent.
  • one or more oxidative pulp modifiers are present from about 1 weight percent to 20 weight percent.
  • the composition includes about 5 weight percent to about 15 weight percent of one or more oxidative pulp modifiers.
  • Representative oxidative pulp modifiers include percarbonates, perborates, hydrogen peroxide, activated hydrogen peroxide, organic peroxyacids and salts thereof, dioxiranes, halogenamines, inorganic peroxides, superoxides and peroxide-superoxides, inorganic peroxyacids and salts thereof, peroxyhydrates, water- soluble organic peroxides, nitrosodisulfonates, hypochlorites, hypobrom ⁇ tes, chlorites, chlorates, bromates, perchlorates, chlorine dioxide, chloroamines, chloroamides, chlorosulfamides, bromoamines, bromoamides, bromosulfamides, chlorosulfonic acid, bromosulfonic acid, chlorine, the like, and combinations thereof.
  • the oxidative pulp modifier may be used in combination with one or more "activators.”
  • the activators include compositions that enhance the effect of the oxidizing agent through catalysis of the oxidation reaction, change in pH, or both.
  • Representative activators include, but are not limited to phosphoric acid; monosodium phosphate; monosodium sulfate; monosodium carbonate; TEMPO (2,2,6,6- tetramethylpiperydidnyoloxyl); 4-hydroxy-TEMPO; ammonium molybdate; tetraacetylethylenediamine (TAED); and pH-changing chemicals affecting oxidation rates, such as acetic acid.
  • alkali typically strengthens the paper product at the expense of decreasing its brightness.
  • the invention includes use of alkali or other pH-controiling chemicals.
  • the composition and method of the invention have the benefit of enabling use of such alkali or pH-controlling chemicals to increase mechanical strength of the paper product without reducing its brightness.
  • Representative pH-controlling chemicals include trisodium phosphate, sodium metaborate, ammonium carbonate, sodium hydroxide, potassium hydroxide, lithium hydroxide, tetramethylammonium hydroxide, ammonium hydroxide, magnesium hydroxide, magnesium carbonate, sodium silicate, sodium carbonate, the like, and combinations thereof.
  • the composition includes about 5 weight percent to about 90 weight percent of the pH-controlling chemical.
  • a more preferred range of one or more pH- controlling chemicals in the composition is from about 20 weight percent to about 50 weight percent.
  • composition may include other organic and inorganic compounds, for example, salts, solvents, and/or wetting agents as needed in certain applications. Any other such compounds may be included without varying from the scope of the invention.
  • the composition may be applied onto wood chips or pulp material to prepare the material for mechanical pulping (e.g., in a chip silo, conveyer belt, or atmospheric steaming bean) or during mechanical pulping (e.g., grinding, refining).
  • the components can be applied separately at different stages of the process. For example, a surfactant may be contacted with the wood chips on the conveyor belt and a reductive pulp modifier may be introduced to the pulp material during refining.
  • the preferred way to implement the method of the invention is in a single formulation before or during the mechanical pulping process.
  • composition may be applied by any means available, such as spraying on wood chip stock, mixing with the liquor (i.e., dilution water), applying with steam (e.g., in a refiner via steam tubes), the like, and combinations thereof.
  • liquor i.e., dilution water
  • steam e.g., in a refiner via steam tubes
  • the composition of the invention is directly fed into the refiner at the mechanical pulping stage.
  • the method includes contacting the pulp material with about 0.001 weight percent to about 5 weight percent of the alkyl alcohol alkoxylate surfactant (as explained in more detail above), based on oven-dry pulp. More preferably, the surfactant level is from about 0.003 weight percent to about 0.2 weight percent, based on oven-dry pulp. The most preferred surfactant level is from about 0.005 weight percent to 0.1 weight percent, based on oven-dry pulp.
  • the method includes introducing to the pulp material about 0.005 weight percent to about 5 weight percent of one or more reductive pulp modifiers (as explained in more detail above), based on oven-dry pulp.
  • the reductive pulp modifier is added from about 0.01 weight percent to about 0.5 weight percent, based on oven-dry pulp.
  • one or more reductive pulp modifiers are added from about 0.02 weight percent to about 0.1 weight percent, based on oven-dry pulp.
  • the method includes introducing to the pulp material about 0.01 weight percent to about 5 weight percent of one or more oxidative pulp modifiers, based on oven-dry pulp.
  • a preferred level of the oxidative pulp modifier is from about 0.01 weight percent to about 0.5 weight percent, based on oven-dry pulp.
  • a most preferred dosage of one or more oxidative pulp modifiers from about 0.02 weight percent to about 0.1 weight percent, based on oven-dry pulp.
  • the level of pH-controlling chemical may vary depending upon the pH requirements or pH of the system. These embodiments include introducing to the pulp material (as stated, either separately or mixed with one or more other components of the composition) from about 0.05 weight percent to about 10 weight percent of one or more pH-controlling chemicals, based on oven-dry pulp. In one embodiment, the pH-controlling chemicals are introduced from about 0.1 weight percent to about 2 weight percent, based on oven-dry pulp. In a preferred embodiment, the pH-controlling chemicals are used from about 0.4 weight percent to about 1 weight percent, based on oven-dry pulp.
  • compositions used in the following examples are listed below. All percentages are in weight percent, unless indicated otherwise.
  • Composition A about 14.5% chelant, about 17.5% hydrotrope, and about 3% surfactant.
  • Composition Al about 0.15% chelant and about 0.15% Composition A.
  • Composition B about 5.4% chelant, about 15.2% hydrotrope, about 1.3% surfactant, and about 16.2% reductive pulp modifier.
  • Composition Bl about 0.3% Composition A and about 0.2% reductive pulp modifier.
  • Composition C about 0.3% Composition A, about 0.2% reductive pulp modifier, and about 2% pH-controlling chemical.
  • Composition Cl about 0.3% Composition A, about 0.2% reductive pulp modifier, and about 1% trisodium phosphate (Na 3 PO 4 ).
  • Composition C2 about 0.3% Composition A, about 0.2% reductive pulp modifier, and about 0.5% pH-controlling chemical.
  • Composition D about 0.5% Composition B and about 0.5% NaOH.
  • Composition E about 0.3% Composition A, about 0.2% reductive pulp modifier, and about 0.5% pH-controlling chemical.
  • Composition F about 0.3% Composition A, about 0.2% reductive pulp modifier, and about 1% sodium metaborate (NaBO 2 ).
  • Composition G about 0.5% Composition A and about 1% oxidative pulp modifier.
  • Composition H about 0.5% Composition A and about 1% oxidative pulp modifier.
  • Composition I about 0.3% Composition A, about 0.2% reductive pulp modifier, about 0.25% alkali, and about 0.25% pH-controlling chemical.
  • Composition J about 0.3% Composition A, about 0.2% reductive pulp modifier, and about 0.5% pH-controlling chemical.
  • xv. Composition K about 16% surfactant xvi.
  • Composition L about 24% pH-controlling chemical, about 2% chelant, and about 9.5% reductive pulp modifier.
  • Composition M about 0.1% Composition L and about 0.5% sodium hydroxide.
  • Composition N about 24% pH-controlling chemical, about 2% chelant, and about 9.5% sodium sulfite.
  • Composition O about 0.5% Composition N and about 0.5% sodium hydroxide.
  • Pulp material was typically mixed with the composition and may be heated and cooked in a digester at between about 12O 0 C and about 150 0 C.
  • Alternative methods of heating include preheating in a microwave at about 80 0 C, heating with infrared energy, or by heating using any suitable means.
  • the digested pulp may subsequently be refined in a PFI mill running from about 2,000 RPM to about 20,000 RPM, depending on the setting.
  • the treated pulp was diluted with deionized water to 5 percent consistency and then dewatered to 20 percent consistency.
  • the dewatered pulp was bleached at 10 percent consistency at 70 0 C for about 1 hour with from 2.5 to 3 weight percent H 2 O 2 , about 2 weight percent NaOH, and optionally about 1.13 weight percent sodium silicate.
  • Handsheets were made using a B ⁇ chner funnel (5 gram o.d. pulp, 015 cm, pressed and air-dried) and/or a Noble&Wood handsheet mold (8 in 2 , 60 g/m 2 ). Brightness was measured using Elrepho and Technodyne instruments (ISO Brightness - R457). All percentages are weight percent of the product to o.d. pulp.
  • TMP GWD-rejects, cooked and digested for 20 min at 15O 0 C in a microwave, PFI mill 20,000 RPM (reduced-force beating), bleached with 2.5% H 2 O 2 . Brightness measurements are shown in Table I below.
  • CTMP GWD-rejects, 1.8% sodium sulfite added to the pulp, cooked and digested for 20 min at 150 0 C in microwave, PFI mill 20,000 RPM (reduced-force beating), initial pH 8.1, bleached with 2.5% H 2 O 2 . Freeness (CSF, ml) and brightness measurements are shown in Table II.
  • FiberBrite® 03PO054 (“FB03") is a pulp brightness enhancer available from Nalco Company® in Naperville, IL.
  • CTMP TMP-accepts, 0.5% NaOH and 1% Na 2 SO 3 added to the pulp material, cooked and digested for 15 min at 12O 0 C; PFI mill 1,000 RPM, bleached with 2.5% H 2 O 2 . Brightness data are shown in Table III.
  • CTMP TMP-accepts, 0.5% NaOH and 1% Na 2 SO 3 added to the pulp material, cooked and digested for 15 min at 120 0 C 5 PFI mill at 2,000 RPM, bleached with 2.5% H 2 O 2 .
  • Brightness, burst index (kPa-m 2 /g), and tensile index (Nm/g) are shown in Table IV. This example illustrates minimized brightness loss at the mechanical pulping stage in presence of alkali that was used to improve mechanical properties of handsheets made of bleached pulp.
  • TMP TMP-accepts, cooked and digested for 15 min at 12O 0 C, PFI mill at 6000 RPM, bleached with 4% H 2 O 2 .
  • Original pH pH (pH-A), pH after PFI mill (pH-B), brightness measurements, burst index (kPa-m 2 /g), and tensile index (Nm/g) are shown in Table V.
  • Unbleached pulp had a brightness of 50.09.
  • TMP GWD-rejects, cooked and digested for 15 min at 120 0 C, PFI milled at 20,000 RPM, bleached with 2.5% H 2 O 2 .
  • Original pH (pH-A), pH after PFI mill (pH-B), brightness measurements, burst index (kPa-m 2 /g), and tensile index (Nm/g) are shown in Table VI.
  • Moderate alkaline buffering combined with other components of the composition led to marked improvements in brightness and mechanical integrity.
  • Such buffering is possible with trisodium phosphate or sodium metaborate that are potential alternatives to standard alkalization with sodium hydroxide.
  • Sodium hydroxide provides higher strength, but more moderate buffering provides higher brightness. Alkalization normally negatively affects brightness, and the proposed compositions compensate for this deficiency.
  • TMP TMP-accepts, cooked and digested for 15 min at 12O 0 C, PFI mill at 6,000 RPM, bleached with 4% H 2 O 2 .
  • Original pH (pH-A), pH after PFI mill (pH-B), brightness measurements, burst index (kPa-mVg), and tensile index (Nm/g) are shown in Table VlI
  • trisodium phosphate is affecting strength only at high concentrations. Metaborate is more efficient at the same dose.
  • the data also show that combined application of the new chemistry with oxidants-alkaline buffers such as perborate and especially percarbonate provides significant improvement.
  • Table VII Table VII
  • TMP GWD-rejects, cooked and digested for 15 min at 120 0 C, PFI mill at 10,000 RPM, bleached with 3% H 2 O 2 , 1.13% sodium silicate added to the pulp. Comparative brightness measurements, burst index (kPa-m 2 /g), and tensile index (Nm/g) are shown in Table VIII.
  • TMP GWD-rejects, cooked and digested for 15 min at 120 0 C, PFI mill at 4,000 RPM, pulp material dosed with PAA and H 2 O2 dosed as actives and Composition B as product, bleached at 7O 0 C for 1 hour with 3% H 2 O 2 and 2% NaOH.
  • Table IX shows unbleached and bleached brightness and tensile index (Nm/g).
  • TMP GWD-rejects, cooked and digested for 5 min at 12O 0 C, PFI mill at 4,000 RPM, pulp material dosed with PAA and H 2 O 2 as actives and Composition B as product, bleached at 7O 0 C for 1 hour with 3% H 2 O 2 and 2% NaOH.
  • Table X shows bleached brightness and tensile index (Nm/g).
  • composition A Prototype product for CTMP applications was evaluated.
  • the composition was applied at a rate of 6 lb/ton o.d. wood chips.
  • the composition was applied at the refining stage, and its effect was followed during the multi-stage refining-bleaching process.
  • the evaluation demonstrated a possibility of caustic removal at the refining stage without any negative effect on paper strength, freeness, shives, or energy consumption.
  • Composition A also produced improvement in brightness and higher efficiency in the first stage bleaching and lesser peroxide consumption in the second stage bleaching.
  • Composition A was applied at the impregnation refining stage, cutting peroxide by 14 kg/ton at the second stage, bleaching did not negatively affect brightness, which was even higher than under normal conditions.
  • Application of the composition at the refining stage provided 10 percent energy savings that, when the same energy was applied, resulted in a 10 percent productivity increase.
  • compositions B, K, and M Prototype products from TMP applications.
  • Composition K was applied at the rate of 1 lb/ton (0.45 weight percent) and sodium hydroxide at 0.5 weight percent to o.d. wood at the refiner stage. Freeness reduction was observed with each prototype ranging from 4 percent (8 ml drop) to 9.7 percent (20 ml drop).
  • Brightness of unbleached pulp increased with Composition B by 1.0 point and 1.2 points (at 2 lb/ton dose). The gain in brightness of bleached pulp, which was not directly measured, was expected to be greater than that observed in the unbleached pulp. Breaking length, tensile strength, and tensile energy absorption ("TEA") all improved, with TEA increasing up to 24 percent.
  • TMP tensile strength, and tensile energy absorption

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Abstract

L'invention porte sur une composition et une méthode améliorant le processus de production de la pâte mécanique en diminuant la mobilité et la quantité des anas, et permettant des économies en énergie et en produits chimiques tout en augmentant la brillance et la résistance mécanique d'un produit papetier. La composition inclut des formulations, telles que des surfactants, des chélants, des hydrotropes, des modificateurs de pâte, des réducteurs et oxydants et des produits chimiques régulant le pH. La méthode consiste à introduire sélectivement ces formulations dans la pâte au cours du processus mécanique de formation de la pâte.
PCT/US2007/083461 2006-11-03 2007-11-02 Composition et méthode améliorant la qualité des fibres et l'efficacité du processus de production de pâte mécanique WO2008058003A2 (fr)

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CA2668158A CA2668158C (fr) 2006-11-03 2007-11-02 Composition et methode ameliorant la qualite des fibres et l'efficacite du processus de production de pate mecanique
EP07844840.4A EP2082093B1 (fr) 2006-11-03 2007-11-02 Composition et méthode améliorant la qualité des fibres et l'efficacité du processus de production de pâte mécanique
CN2007800410428A CN101535561B (zh) 2006-11-03 2007-11-02 用于改进机械制浆中纤维质量和工艺效率的方法和组合物
AU2007317407A AU2007317407A1 (en) 2006-11-03 2007-11-02 Method and composition for improving fiber quality and process efficiency in mechanical pulping
BRPI0716279-0A2A BRPI0716279A2 (pt) 2006-11-03 2007-11-02 Composição que melhora um processo mecânico de formação de polpa e método para melhorar um processo mecânico de formação de polpa

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US11/556,259 2006-11-03
US11/556,259 US20080105392A1 (en) 2006-11-03 2006-11-03 Method and composition for improving fiber quality and process efficiency in mechanical pulping

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US9656914B2 (en) 2013-05-01 2017-05-23 Ecolab Usa Inc. Rheology modifying agents for slurries
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EP3059056A1 (fr) 2015-02-23 2016-08-24 Basf Se Procédé de fabrication de fibres de bois et panneaux en fibres de bois
CA3001717A1 (fr) 2015-10-15 2017-04-20 Ecolab Usa Inc. Cellulose nanocristalline et cellulose nanocristalline greffee avec un polymere comme agents de modification de la rheologie pour suspensions d'oxyde de magnesium et de chaux
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EP2082093B1 (fr) 2018-12-26
TW200833901A (en) 2008-08-16
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CN101535561A (zh) 2009-09-16
CA2668158A1 (fr) 2008-05-15
CA2668158C (fr) 2013-09-03
US20080105392A1 (en) 2008-05-08
AU2007317407A1 (en) 2008-05-15
CN101535561B (zh) 2013-11-06
WO2008058003A3 (fr) 2008-07-03
EP2082093A4 (fr) 2010-08-04
CL2007003178A1 (es) 2008-07-11
US8262852B2 (en) 2012-09-11
US20100269993A1 (en) 2010-10-28

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